Prediction of micromixing effects in precipitation: Case of double‐jet precipitators
Identifieur interne : 002D16 ( Main/Merge ); précédent : 002D15; suivant : 002D17Prediction of micromixing effects in precipitation: Case of double‐jet precipitators
Auteurs : René David [France] ; Bruno Marcant [France]Source :
- AIChE Journal [ 0001-1541 ] ; 1994-03.
English descriptors
- KwdEn :
- Aiche, Aiche journal, Average crystal size, Average size, Barium, Barium sulfate, Barium sulphate precipitation, Base case zone, Bulk fluid, Calcium oxalate monohydrate, Chem, Chemical reaction, Circulation time, Crystal number, Crystal size, Diffusional growth, Entire feedstocks, Entire tank, Experimental conditions, Experimental results, Feed location, Feed locations, Feed points, Feed rate, Feed streams, Feed tubes, Final distribution, Final volume, Flow rates, High turbulence region, Initial fraction volume, Initial volume, Marcant, Micromixing, Micromixing effects, Molecular level, Nucleation, Nucleation efficiency, Nucleation flux, Nucleation rate, Other hand, Other processes, Oxalate, Precipitation, Precipitator, Primary nucleation, Primary nucleation flux, Primary nucleation rate, Reactant, Reactive species, Same conditions, Secondary nucleation, Semibatch, Significant consumption, Space time, Sulfate, Supersaturation, Tank reactors, Tosun, Total nucleation flux, Turbulence region, Turbulent region, Volume ratio.
- Teeft :
- Aiche, Aiche journal, Average crystal size, Average size, Barium, Barium sulfate, Barium sulphate precipitation, Base case zone, Bulk fluid, Calcium oxalate monohydrate, Chem, Chemical reaction, Circulation time, Crystal number, Crystal size, Diffusional growth, Entire feedstocks, Entire tank, Experimental conditions, Experimental results, Feed location, Feed locations, Feed points, Feed rate, Feed streams, Feed tubes, Final distribution, Final volume, Flow rates, High turbulence region, Initial fraction volume, Initial volume, Marcant, Micromixing, Micromixing effects, Molecular level, Nucleation, Nucleation efficiency, Nucleation flux, Nucleation rate, Other hand, Other processes, Oxalate, Precipitation, Precipitator, Primary nucleation, Primary nucleation flux, Primary nucleation rate, Reactant, Reactive species, Same conditions, Secondary nucleation, Semibatch, Significant consumption, Space time, Sulfate, Supersaturation, Tank reactors, Tosun, Total nucleation flux, Turbulence region, Turbulent region, Volume ratio.
Abstract
Mixing effects are evaluated for double jet semibatch and continuous stirred precipitators by a model which gives the variation of the primary nucleation flux from the mixing conditions. The predicted trends are compared with results of various authors, including those from a new study of calcium oxalate semibatch double‐jet precipitation. Satisfactory qualitative agreement is found for the different chemical systems as a function of feed rate, stirring speed and feed locations for calcium oxalate precipitation. Two types of precipitation systems are demonstrated, depending on the ratio added/tank volume, the initial supersaturations and the intrinsic stiffness factor of a given precipitation. The difference between the two types depends on the increase or reduction of the primary nucleation flux by imperfect mixing with respect to the reference primary nucleation flux obtained with perfect mixing.
Url:
DOI: 10.1002/aic.690400306
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ISTEX:DCDE3C8815A9D04A717F10818527E5945396B367Le document en format XML
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<term>Average size</term>
<term>Barium</term>
<term>Barium sulfate</term>
<term>Barium sulphate precipitation</term>
<term>Base case zone</term>
<term>Bulk fluid</term>
<term>Calcium oxalate monohydrate</term>
<term>Chem</term>
<term>Chemical reaction</term>
<term>Circulation time</term>
<term>Crystal number</term>
<term>Crystal size</term>
<term>Diffusional growth</term>
<term>Entire feedstocks</term>
<term>Entire tank</term>
<term>Experimental conditions</term>
<term>Experimental results</term>
<term>Feed location</term>
<term>Feed locations</term>
<term>Feed points</term>
<term>Feed rate</term>
<term>Feed streams</term>
<term>Feed tubes</term>
<term>Final distribution</term>
<term>Final volume</term>
<term>Flow rates</term>
<term>High turbulence region</term>
<term>Initial fraction volume</term>
<term>Initial volume</term>
<term>Marcant</term>
<term>Micromixing</term>
<term>Micromixing effects</term>
<term>Molecular level</term>
<term>Nucleation</term>
<term>Nucleation efficiency</term>
<term>Nucleation flux</term>
<term>Nucleation rate</term>
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<term>Other processes</term>
<term>Oxalate</term>
<term>Precipitation</term>
<term>Precipitator</term>
<term>Primary nucleation</term>
<term>Primary nucleation flux</term>
<term>Primary nucleation rate</term>
<term>Reactant</term>
<term>Reactive species</term>
<term>Same conditions</term>
<term>Secondary nucleation</term>
<term>Semibatch</term>
<term>Significant consumption</term>
<term>Space time</term>
<term>Sulfate</term>
<term>Supersaturation</term>
<term>Tank reactors</term>
<term>Tosun</term>
<term>Total nucleation flux</term>
<term>Turbulence region</term>
<term>Turbulent region</term>
<term>Volume ratio</term>
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<term>Average crystal size</term>
<term>Average size</term>
<term>Barium</term>
<term>Barium sulfate</term>
<term>Barium sulphate precipitation</term>
<term>Base case zone</term>
<term>Bulk fluid</term>
<term>Calcium oxalate monohydrate</term>
<term>Chem</term>
<term>Chemical reaction</term>
<term>Circulation time</term>
<term>Crystal number</term>
<term>Crystal size</term>
<term>Diffusional growth</term>
<term>Entire feedstocks</term>
<term>Entire tank</term>
<term>Experimental conditions</term>
<term>Experimental results</term>
<term>Feed location</term>
<term>Feed locations</term>
<term>Feed points</term>
<term>Feed rate</term>
<term>Feed streams</term>
<term>Feed tubes</term>
<term>Final distribution</term>
<term>Final volume</term>
<term>Flow rates</term>
<term>High turbulence region</term>
<term>Initial fraction volume</term>
<term>Initial volume</term>
<term>Marcant</term>
<term>Micromixing</term>
<term>Micromixing effects</term>
<term>Molecular level</term>
<term>Nucleation</term>
<term>Nucleation efficiency</term>
<term>Nucleation flux</term>
<term>Nucleation rate</term>
<term>Other hand</term>
<term>Other processes</term>
<term>Oxalate</term>
<term>Precipitation</term>
<term>Precipitator</term>
<term>Primary nucleation</term>
<term>Primary nucleation flux</term>
<term>Primary nucleation rate</term>
<term>Reactant</term>
<term>Reactive species</term>
<term>Same conditions</term>
<term>Secondary nucleation</term>
<term>Semibatch</term>
<term>Significant consumption</term>
<term>Space time</term>
<term>Sulfate</term>
<term>Supersaturation</term>
<term>Tank reactors</term>
<term>Tosun</term>
<term>Total nucleation flux</term>
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<front><div type="abstract" xml:lang="en">Mixing effects are evaluated for double jet semibatch and continuous stirred precipitators by a model which gives the variation of the primary nucleation flux from the mixing conditions. The predicted trends are compared with results of various authors, including those from a new study of calcium oxalate semibatch double‐jet precipitation. Satisfactory qualitative agreement is found for the different chemical systems as a function of feed rate, stirring speed and feed locations for calcium oxalate precipitation. Two types of precipitation systems are demonstrated, depending on the ratio added/tank volume, the initial supersaturations and the intrinsic stiffness factor of a given precipitation. The difference between the two types depends on the increase or reduction of the primary nucleation flux by imperfect mixing with respect to the reference primary nucleation flux obtained with perfect mixing.</div>
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